SE7413670L - KIT FOR REFINING RAKADMIUM AND DEVICE FOR IMPLEMENTING THE KIT. - Google Patents
KIT FOR REFINING RAKADMIUM AND DEVICE FOR IMPLEMENTING THE KIT.Info
- Publication number
- SE7413670L SE7413670L SE7413670A SE7413670A SE7413670L SE 7413670 L SE7413670 L SE 7413670L SE 7413670 A SE7413670 A SE 7413670A SE 7413670 A SE7413670 A SE 7413670A SE 7413670 L SE7413670 L SE 7413670L
- Authority
- SE
- Sweden
- Prior art keywords
- leg
- tube
- condenser
- transition portion
- crude
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B17/00—Obtaining cadmium
- C22B17/06—Refining
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B19/00—Obtaining zinc or zinc oxide
- C22B19/04—Obtaining zinc by distilling
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B9/00—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
- C22B9/04—Refining by applying a vacuum
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
1441736 Refining cadmium PREUSSAG A G METALL 25 Oct 1974 [13 April 1974] 46308/74 Heading C7D Crude cadmium is continuously refined by evaporation in a vacuum and passing the vapour through a reflex condenser to remove the higher boiling point impurities prior to condensing and collecting the purified Cd. The apparatus used comprises an inverted U-shaped steel vacuum chamber 20, with a first and second legs formed by an inclined transition portion 34. In the first e.g., an evaporator portion 22 with a heating jacket 28 leads to a reflex condenser 30 containing a helical baffle 56 and surrounded by a temperature adjustable jacket 32. The outlet of the reflex condenser 30 connects with transition portion 34 which is connected to a condenser 36 in the second leg. A temperature adjustable jacket 38 surrounds condenser 36. A vacuum tube 42, connected to a pump, extends to just above the outlet end of the second leg and has the largest possible diameter to permit a minimum annular space 50 between the tube 42 and the wall of chamber 20 to give the maximum condensing surface. The free end of the second leg feeds via pipe 44 into a heated receiver 46. The crude liquid Cd input to the first leg is from a heated vessel 10 through tube 12, a further tube 16 leading from the first leg to a heated distillation residue container 14, the heights of tubes 12 and 16 being arranged such that the residue cannot feed back into the input tube. The materials in vessels 10, 14 and 46 act as barometric locks. In operation, the pressure and temperatures are adjusted and crude Cd is sucked into evaporator 22 via tube 12. The evaporated vapour passes into the baffled reflex condenser where impurities and some Cd condense and flow back counter current to the ascending vapour, this further purifying the gas. The distillation residue is discharged into receiver 14. The remaining gas passes through the transition portion 34 into condenser 36 in the second leg where it is condensed and collected in vessel 46.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE2418170A DE2418170C2 (en) | 1974-04-13 | 1974-04-13 | Process and apparatus for refining crude cadmium |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| SE7413670L true SE7413670L (en) | 1975-10-14 |
| SE401374B SE401374B (en) | 1978-05-02 |
Family
ID=5912969
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SE7413670A SE401374B (en) | 1974-04-13 | 1974-10-30 | RAKADMIUM REFINING KIT AND DEVICE PERFORMANCE DEVICE |
Country Status (11)
| Country | Link |
|---|---|
| JP (1) | JPS548535B2 (en) |
| BE (1) | BE820375A (en) |
| CA (1) | CA1022344A (en) |
| DE (1) | DE2418170C2 (en) |
| ES (2) | ES430654A1 (en) |
| FI (1) | FI60036C (en) |
| GB (1) | GB1441736A (en) |
| IT (1) | IT1019296B (en) |
| NL (1) | NL182328C (en) |
| NO (1) | NO136799C (en) |
| SE (1) | SE401374B (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS578853B2 (en) * | 1974-05-14 | 1982-02-18 | ||
| FR2398807A1 (en) * | 1977-07-29 | 1979-02-23 | Preussag Ag Metall | Impure cadmium refined by vacuum distillation - using an inverted U-tube still |
| CN100494424C (en) * | 2007-08-31 | 2009-06-03 | 侯仁义 | Hydrogenation method for high-pure cadmium |
| CN108570564B (en) * | 2018-07-09 | 2023-11-17 | 长沙科力威蒸馏技术有限公司 | Vacuum distillation furnace |
| WO2020017202A1 (en) | 2018-07-18 | 2020-01-23 | パナソニックＩｐマネジメント株式会社 | Electric tool, control method, and program |
| CN112322913A (en) * | 2020-12-10 | 2021-02-05 | 中国核电工程有限公司 | Refining device and refining method |
-
1974
- 1974-04-13 DE DE2418170A patent/DE2418170C2/en not_active Expired
- 1974-09-16 IT IT5304874A patent/IT1019296B/en active
- 1974-09-24 NO NO743438A patent/NO136799C/en unknown
- 1974-09-25 FI FI2791/74A patent/FI60036C/en active
- 1974-09-26 BE BE148927A patent/BE820375A/en not_active IP Right Cessation
- 1974-10-03 ES ES430654A patent/ES430654A1/en not_active Expired
- 1974-10-03 ES ES430655A patent/ES430655A1/en not_active Expired
- 1974-10-15 NL NL7413532A patent/NL182328C/en not_active IP Right Cessation
- 1974-10-25 GB GB4630874A patent/GB1441736A/en not_active Expired
- 1974-10-30 SE SE7413670A patent/SE401374B/en not_active IP Right Cessation
- 1974-10-30 JP JP12452774A patent/JPS548535B2/ja not_active Expired
- 1974-11-04 CA CA213,101A patent/CA1022344A/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| NO743438L (en) | 1975-10-14 |
| JPS548535B2 (en) | 1979-04-17 |
| NO136799C (en) | 1977-11-09 |
| DE2418170B1 (en) | 1975-02-20 |
| NL7413532A (en) | 1975-10-15 |
| JPS50133923A (en) | 1975-10-23 |
| SE401374B (en) | 1978-05-02 |
| NL182328C (en) | 1988-02-16 |
| FI60036B (en) | 1981-07-31 |
| ES430654A1 (en) | 1976-10-16 |
| GB1441736A (en) | 1976-07-07 |
| FI279174A (en) | 1975-10-14 |
| NL182328B (en) | 1987-09-16 |
| AU7544574A (en) | 1976-05-20 |
| CA1022344A (en) | 1977-12-13 |
| NO136799B (en) | 1977-08-01 |
| ES430655A1 (en) | 1976-10-16 |
| DE2418170C2 (en) | 1975-11-06 |
| FI60036C (en) | 1981-11-10 |
| BE820375A (en) | 1975-01-16 |
| IT1019296B (en) | 1977-11-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| IT1008172B (en) | IMPROVEMENT IN VAPOR COMPRESSION DISTILLATION PLANTS | |
| SE7413670L (en) | KIT FOR REFINING RAKADMIUM AND DEVICE FOR IMPLEMENTING THE KIT. | |
| JPS6019746A (en) | Mild distillation for fatty acid | |
| Williams | A binary mixture for evaluating low pressure distillation columns | |
| US1969793A (en) | Concentrator apparatus | |
| US2239371A (en) | Separation of metals by distillation | |
| GB614388A (en) | Improvements relating to fractional distillation | |
| US3395083A (en) | Laboratory distilling apparatus | |
| US1628829A (en) | Process of distilling hydrochloric acid | |
| SU177069A1 (en) | APPARATUS FOR CONTINUOUS METAL REFINING | |
| US3457142A (en) | Multi-stage flash evaporators having baffle means and a vent in the condenser | |
| US3372096A (en) | High purity water flash evaportator with series stages for redistillation of distillate | |
| Hickman | High vacuum distillation | |
| GB737570A (en) | Improvements in or relating to the recovery of glycerol from industrial liquors by evaporation | |
| GB656605A (en) | Improvements in or relating to apparatus for evaporating liquids | |
| GB828664A (en) | Improvements in or relating to condensation systems | |
| SU143780A1 (en) | The method of fractionation of high-boiling compounds | |
| US3923424A (en) | Self-cleansing diffusion pump | |
| SU1790621A3 (en) | Mercury refining plant | |
| GB769459A (en) | Improved method and apparatus for the purification of liquids by evaporation | |
| US4170522A (en) | Fluid refining method | |
| SU455157A1 (en) | Alkali Metal Distillation Unit | |
| SU990247A1 (en) | Apparatus for cleaning liquids by distillation | |
| US881806A (en) | Process of removing chlorin from raw bromin. | |
| US4201629A (en) | Fluid refining apparatus |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| NUG | Patent has lapsed |
Ref document number: 7413670-6 Effective date: 19920510 Format of ref document f/p: F |